US2015218720A1PendingUtilityA1
Process for treating magnesium-bearing ores
Est. expiryAug 24, 2032(~6.1 yrs left)· nominal 20-yr term from priority
Y02P10/20C22B 4/02C22B 3/42C01G 49/08C22B 4/04C22B 26/22C22B 26/20C22B 3/46C22B 23/0461C25C 7/06C22B 21/0015C22B 3/44C25C 3/04C01G 49/06C22B 3/10C25C 1/08
49
PatentIndex Score
0
Cited by
0
References
0
Claims
Abstract
It is described a process for extracting magnesium from magnesium-bearing materials comprising the steps of leaching the magnesium-bearing material with HCl as to obtain a leachate comprising the magnesium in solution and a solid form; purify said leachate to produce magnesium chloride and electrolysing the magnesium chloride producing magnesium metal.
Claims
exact text as granted — not AI-modified1 . A process for extracting magnesium metal from a magnesium-bearing material, said process comprising:
a. leaching the magnesium-bearing material with HCl as to obtain a leachate containing magnesium chloride; and b. electrolyzing the magnesium chloride for extracting magnesium metal.
2 . The process of claim 1 , wherein the step of electrolyzing the magnesium chloride comprises using an electrolysis cell having a cathode and an anode wherein a source of hydrogen gas is delivered to the anode.
3 . The process of claim 2 , further comprising the step of dehydrating magnesium chloride contained in the leachate before the step of electrolyzing the leachate containing magnesium chloride to obtain magnesium metal.
4 . The process of claim 3 , wherein a two step fluidized bed is used for dehydrating the magnesium chloride.
5 . The process of claim 4 , further comprising a drying step in a fluidized bed dryer followed by gaseous HCl drying to extract anhydrous magnesium chloride.
6 . The process of claim 5 , wherein the dehydrated magnesium chloride is further dissolved in molten salt electrolyte.
7 . The process of claim 1 , wherein dry hydrochloric acid is added to proceed with the dehydration step.
8 . The process of claim 1 , further comprising recycling said gaseous HCl by contacting it with water so as to obtain a composition having a concentration of about 25 to about 45 weight % and using said composition for leaching.
9 . The process of claim 8 , wherein said magnesium-bearing material is leached with HCl having a concentration of about 20 to about 45 weight % at a temperature of about 60 to about 125° C.
10 . (canceled)
11 . The process claim 8 , wherein said recycled gaseous HCl so-produced is contacted with water so as to obtain said composition having a concentration between 25 and 36 weight %.
12 . (canceled)
13 . The process of claim 1 , further comprising the step of passing the leachate on a chelating resin system to recuperate nickel chloride from said leachate.
14 . (canceled)
15 . The process of claim 13 , further comprising the step of electrolyzing the nickel chloride to obtain nickel.
16 . The process of claim 1 , further comprising the step of hydrolysis at low temperature of about 155 to about 350° C. the leachate to extract hematite.
17 . The process of claim 16 , further comprising the step of passing the hydrolyzed leachate on a chelating resin system to recuperate nickel chloride from said hydrolyzed leachate.
18 . (canceled)
19 . The process of claim 1 , further comprising the step of supplementing at least one of MgCO 3 , H 2 SO 4 , and MgSO 4 to the leachate and purifying said supplemented leachate to recuperate CaCO 3 and/or CaSO 4 .
20 . The process of claim 13 , further comprising the step of separating a liquid phase from a solid form of the leachate and concentrating said liquid phase to a concentrated liquid having an iron chloride concentration of at least 30% by weight; and then said iron chloride is hydrolyzed at a temperature of about 155 to about 350° C. while maintaining a ferric chloride concentration at a level of at least 65% by weight, to generate a composition comprising a liquid and precipitated hematite, and recovering said hematite.
21 . (canceled)
22 . (canceled)
23 . The process of claim 1 , further comprising a step of magnetic separation of the magnesium-bearing material before step a) of leaching to recover magnetite.
24 . The process of claim 1 , further comprising the steps of oxidizing reacted leachate and crystallizing said reacted leachate to recover Fe 2 O 3 and AlCl 3 .
25 . (canceled)
26 . (canceled)
27 . (canceled)
28 . (canceled)
29 . (canceled)
30 . The process of claim 1 , wherein the magnesium-bearing material is a magnesium-bearing ore.
31 . (canceled)
32 . The process of claim 1 , wherein the magnesium-bearing material is an asbestos mine tailing.
33 . (canceled)
34 . (canceled)
35 . (canceled)
36 . (canceled)Join the waitlist — get patent alerts
Track US2015218720A1 — get alerts on status changes and closely related new filings.
We store only your email — no account needed. See our privacy policy.